US2394449A

US2394449A - Manufacture of explosives

Info

Publication number: US2394449A
Application number: US468842A
Authority: US
Inventors: Milton L Herzog
Original assignee: Olin Industries Inc
Current assignee: Olin Industries Inc
Priority date: 1942-12-12
Filing date: 1942-12-12
Publication date: 1946-02-05
Anticipated expiration: 1963-02-05

Description

Feb. 5, 1946. M. HERZQG 2,394,449

MANUFACTURE OF EXPLOS IVES Filed Dec. 12, 1942 INVENTOR Mi/ton L. h'er'zog BY ATTORNEY Patented Feb. 5, 1946 srs FFQE MANUFACTURE OF LOSIVES Milton L. Herzog, Glendale, Ma, gnor to Olin Industries, Inc., a corporation of Delaware This invention relates to the manufacture of explosives and more particularly to the manufacture of granular explosives, such as those having a base of nitrocellulose.

One of the objects of this invention is to pro vide a process whereby the treating steps may be controlled so as to secure emcient and economical operation.

Another object is to provide a process whereby the incorporation of additional ingredients such as the usual modifying agents, for instance, deterrents, stabilizers or accelerators, into a granular explosive may be efliciently and readily effected.

Another object is to provide a process in which 4 the removal of solvent from the powder grains is effectively controlled to permit a termination of the treatment at any desired degree of the solvent removal.

Another object is to provide a process in which the operations may be controlled to secure a superior and readily duplicable product.

Another object is to provide a control test for the manufacture of granular explosives, whereby the change in internal structure of the grains can be examined during the processing steps and successive treatments governed thereby.

Another object i to provide efiective means for controllinga treatment to remove volatile liquids from powder grains.

Still another object is to provide effective means for controlling treatments to coat powder grains with deterrents and other modifying agents.

Other objects will become apparent to those skilled in'the art when the following detail description is read inconnection with the accompanying drawing in which Figures 1 to 20 illustrate the appearance, at a magnification of about 50 to l, of sections of certain powder grains prepared in accordance with this invention. r

In accordance with this invention a process is provided for terminating a treatment of explosive grains with a modifying agent at the optimum point, which is determined by examining the change in opacity of the grains during the treatment. l

Although having effective application in the manufacture of other explosive grains, the process of the present invention is particularly suited No. 2,160,626, issued to Schaeier May 30, 1939,

and No. 2,213,255, issued to Olsen et 9.1. September 3, 1940, in which a powder base suspended in water is treated with a water immiscible liquid solvent to form grains and in which the grains may then be treated with various modifying agents in the water suspension.

it has been found according to the present invention that when a granular explosive is treated with modifying agents; such as the usual deterrents. the usual type solvents, nitroglycerine and the like, or mixtures thereof, the degree of coatins. penetration or removal of such modifiers can be readily determined by the degree of transparency shown by the grains. For instance, a uni iormly opaque powder grain, Figure 1, may become translucent throughout, Figure 4, when completely impregnated with such a modifier, or a translucent powder grain will show a difierence in transparency when coated or impregnated with such modifiers depending on the amount of impregnation or coating. Such differences in transparency oi the grain are readily detectable when the powder grains are sectioned and examined in accordance with this invention.

In carrying out the process of this invention, representative grains of the explosives are removed from the mass under treatment, sectioned, and the sections are then examined to determine their opacity. When grains are obtained giving sections showing the opacity necessary for the desired result for the particular treatment underway, the treatment is terminated. This process is of decided advantage since prior methods involving more "or lessextensive chemical analysis have not been found suitable as a means of controlling such treatments and in any event do not give a clear picture as to the internal composition and structure of the explosive grain.

The degree of opacity of the grains indicating that the treatment should be terminated will of course vary with different types and conditions of treatment and with the result desired to be obtained during the treatment. For instance, when powder grains are being impregnated with a liquid modifier and representative grains are periodically removed and sectioned, the first visible eflect of impregnation is usually a ring 2, Figure 2, around the periphery of the section which is more transparent than the center portion I and which usually increases in size 4, Figure 3, as the treatment proceeds until the whole grain attains a uniform transparency. Figure 4. at or before which.

time the treatment may be terminated depending on the result desired. Similarly, when a solvent or other. component is removed from the powder grains, the first visible eflect when successive sections are examined is usually that a less transparent core it, Figure 13, appears atthe center of the grain which increases in size I I, l9, 2! and 23 derway. the grain may have a more or less op que core at the beginning of the treatment which may increase or decrease in size as the treatment proceeds and the treatment is then terminated when the desired change in transparency of the grain is effected. 4

The character of the treatment given and the result desired are the main factors governing the appearance to be attained in the grain section before the treatment is terminated. It has usually been found desirable to have some standard by which the transparency of the grain sections can be measured in order to insure that the treating operation may be terminated at the optimum point. This can readily be accomplished by taking photographs of a series of sections prepared from grains removed periodically during the treatment and thereafter using the photograph .of the section indicating that the treatment should be terminated as a standard for comparison with sections of grains removed from grains undergoing treatment of similar character. It will, of course, be apparent that such a standard photograph can be prepared for each type of treatment used and result desired so that any desired effect can then be accurately duplicated.

The process of this invention is thus'of great advantage when it is desired to leave a definite amount of solvent in powder grains for the purpose of subsequent treatment, or when it is desired to impregnate or coat explosive grains with a modifying agent, or, for instance, when in the interest of economy it is desired to terminate a treatment immediately upon the attainment of a desired result.

The thin sections of the explosive grains may be prepared in any suitable manner provided that care is taken to prevent any surface flow of the various components of the grain. The thickness of the grain section will vary with the degree of opacity of the grain, it being necessar to provide sections thin enough to permit the passage of some light in order to properl examine the grain.

With gelatinous globular powder grains having a diameter in the range of about 0.010 inch to 0.030 inch, a section having a thickness of about 0.0015 inch has usually been found satisfactory. Further, with smaller globular grains a thinner section must be prepared to prevent the high degree of curvature at the edge of the section of disk from acting as a lens and distorting the actual appearance of the section.

The preferred method of preparing the grain sections in accordance with this invention is to first cement the grain to a glass microscope slide with a suitable mounting agent such as an aqueous dispersion of gum arabic and then to remove slightly less than one-half the grain by carefully grinding, for instance on about number 0, grit metallurgical paper, care being used to grind to a flat surface with a reciprocal motion and with substantially no pressure except the weight of the microscope slide in order to prevent surface flow of the constituents of the grain. The flat ground surface of the grain is then polished by a similar grinding operation, for instance with the use of about number 0000 grit metallur ical paper and with a reciprocal motion at right angles to that employed in the coarse grinding. The polishing is continued until all lines on the surface caused b the grinding abrasive have disappeared. The grain is then loosened from the microscope slide for instance by flooding with water, mounted with the flat surface toward the glass, and the above grinding and polishing operation is repeated to give a section or disk of the desired uniform thickness. The section is then ready for examination and since such explosive sections are usually small, a microscope is usually required for the examination.

If, in the preparation of sections of explosive grains, it is desired to use a microtome instead of a grinding operation, extreme-care must be exercised to remove from the surface of the sections all scratches formed by the cutting blade and all displaced components of the grain. Frequently it is impossible to employ such cutting devices, particularly with explosive grains composed of or having relatively plastic components, since it is a characteristic of such devices that the pressure employed in cutting tends to distort the whole section or leave marks in the surface so that upon examination the true nature of the grain is misrepresented by the appearance of the section.

By way of illustration following is a typical embodiment of the present invention in which gelatinized globular powder is treated with nitroglycerine in the presence of a solvent to form doublebase powder and the solvent is then removed from the grains.

About 12.000 pounds of nitrocellulose in the form of gelatinous more or less spherically shaped particles having a diameter of about 0.010 to 0.030

inch, such as maybe prepared according to the 981.9 lbs. toluene. 654.6 lbs.ethyl acetate. 1.75 lbs.

of gum arabic, and 9000 lbs. of water. The suspension is then heated to 65 C. During the entire treatment at 65 C. representative sam les of the powder grains are removed hourly from the suspension for microscopic examination.

As soon as the powder sample is removed from the suspension about 5 grains are cemented to a glass microscope slide with the aid of a 35% aqueous dispersion of gum arable. five grains being used to increase the accuracy of sam ling. The gum arabic is then allowed to dry for about 3 to 5 minutes. The powder grains are then ground to approximately half their original thickness on number 0 grit metallurgical paper, which is held securely and backed by a flat surface. The outer edges of the slide are supported so as to assist in ge erating a flat surface on the powder grains by piling narrow strips of paper on each other to act as a support. and after grinding to a point the mount are carefully dusted with a camel's hair brush in order to remove any adhering pieces of thenumber grinding grit. Aiter the mount has been thoroughly cleaned it is polished on a number 0000 grit metallurgical paper with a reciprocal motion at right angles to the motion employed in the coarse grinding. During the polishing operation the, same light feathery touch is employed as when coarse grinding, with no downward pressure exerted on the slide. The polishing operation is continued pntil all lines on the surface from the number 0 grit have disappeared.

A drop or water is now placed on the mount which after a few seconds will have sufiiciently softened the gum arabic to allow the sections to be lifted from the slide. The sections are transferred to a drop oi water on a clean slide and all particles of grit washed from the polished surfaces. The sections are then cemented to a clean slide with a minute amount of gum arabic with the fiat .side of the samples attached to the glass slide.

final sections having a uniform thickness of about 0.0015 inch.

The sections are then washed thoroughly with water to remove adhering grit particles and are then dried. The drying is preferably accomplished in about minutes by means oi an infrared lamp so adjusted as to produce a temperature of about 50 C. to 55 C. at the surface of the sections. The live sections thus obtained are then examined under the microscope. The total time required in preparing the sections from the time the sample is taken until the microscopic exami nation is completed is usually about 30-45 minutes.

In Figures 1 to 8 are shown representative sections illustrating the change in ap earance of solvent content.

For instance. it it is desired to treat the powder grains described in the above specific example with a deterrent, this may be accomplished .as follows: When sections having the opacity indicated in Figure '7 are obtained, the treatment is terminated by stopping the passage or air through the suspension. raising the temperature of the suspension to about 72 C. and then adding 4 about 1000 pounds of diphenylphthalate emulsithe grains during the treatment at 65 C. The 1 powder grains before the treatment gave an opaque section, Figure 1. After a short period of the treatment with the nltroglycerine and solvent. sections were obtained having a substantially transparent ring 2 around a more or less opaque core 5. As the treatment continued the transparent ring increased in size 5, Figure 3, and the s ze of the core 3 diminished until after about 10 hours treatment the grains were substantially transparent Figure 4, indicating complete impregnation.

At this point air is then bubbled through the suspension to remove the solvent from the powder grains, after a short period of treatment, core 5, Figure 5, became visible, being slightly less trans parent than the ring 8. and as the treatment continued the core became less and less transparent providing an opaque core 7' and substantially transparent ring 8. Further treatment resulted in a core 9 of increased size and transparent ring iii of diminished size, and after about 20 hours a completely opaque grain, Figure 8, was obtained indicating complete removal of the solvent.

In some cases when the powder is to be coated with a deterrent, it is desirable to leave a small amount of the solvent in the powder grains, and this can be readily accomplished by terminatin the treatment when sections are obtained indifled in 2 400 pounds or water at a temperature of C. The temperature or the suspension is maintained at 12 C. until the coating with diphenylphthalate is completed.

The coating of powder with diphenylphthalate or other deterrent may likewise be controlled by theexamination of sections of powder grains removed during the treatment in accordance with this invention. The deterrent coating obtained in the above example appears as a more or less transparent portion enveloping the grain. For instance, a section of a deterrent coated double-base powder grain is shown in Figure 19 in which the deterrent layer is indicated at 2?, the core at 2B. and the intermediate portion composed mostly of nitrocellulose and nitroglycerine at 25. Similarly, a single base powder coated with deterrent is illustrated in Figure 20 in which the deterrent layer is shown at 2% and the core at 28.

In Figures 9 to 18 are shown representative sections of powder grains removed during a treatment oi globular powder with nitroglycerine and solvent, similar to the process described in the specific example above, except that a substantially greater proportion of nitroglycerine was employed. in the treatment, namely about 20% based on the nitrocellulose. The powder grains employed in the treatment were substantially opaque Figure 9. After a short period of treatment, a transparent ring it formed with the core ii and as the treatment continued the transparent ring became larger it andthe core gradually decreased in size It and finally disappeared Figure 12, indicating complete impregnation of the grain. Removal of solvent was then started and after a short period a small core it appeared within the more or less transparent portion id, as contrasted with the relatively large core it of the specific example.

above. As the treatment progressed the. core increased in size, l1, I9, 21 and 28, and the more or less transparent portion diminished, I8, 20, 22 and 24, until substantially opaque sections were obtained, Figure 18, indicating complete removal of the solvent.

Under certain circumstances, depending on the grains being treated and the modifier employed. the grains at the start 01' a treatment may be substantially transparent and no opaque core may be formed during the treatment. in which case the efiect or position of the modifier in the grain can usually be determined by a dark line separating the transparent unaffected portion of the grain from the transparent modified portion of the grain, the dark line being caused by the diil'erence in the refractive index of the modifier and of the substance of the grain. In some instances, however, the effect or position of the modifier in the grain is more easily determined by passing polarized light through the grain sections instead of ordinary light and the process is then carried out by examining the sections with polarized light It should-thus be understood that the appeareating that the powder has the DIQW residual modifier used, conditions of treatment. and nature of the grain being treated, so that no one standard section will serve for all such different treatments. However, having once established the type of modifier, conditions of treatment, etc., capable of giving the result desired, a standard section may be prepared for controlling the treatment and the product can then be readily duplicated by the process of this invention.

By employing the process of this invention as described above, it is possible to obtain a very exact duplication in successive lots of explosive manufactured, and thus greatly improve the uniform quality of the product.

By the terms modifying agents" and "modifiers'as used herein is meant any reagent used in the preparation of a granular explosive, or used to modify or change the characteristics of explosive grains, and having an eilect on the grains detectable when sections of the grains are examined in accordance with this invention. Examples of such modifying agents are the usual accelerators and deterrents used in treating powder and other explosive grains, such as nitroglycerine, dinitrotoluene, dibutylphthalate and substituted ureas; solvents used in preparing and treating powder grains, such as ethyl acetate, toluene, and benzene; and flash inhibitors, stabilizers and moisture profing agents used in the modification of explosive grains.

By the term treatment as used herein with reference to explosive grains is meant any processing step in which a "modifying agent is used in the preparation of a granular explosive, or used to modiiy or change the characteristics of explosive grains. By the terms examination, and examining,

as used herein with reference to thin sections of explosive grains, is meant visual examination of such sections or of photographs, for instance photomicrcgraphs, of such sections. In the case of small sections the visual examination or photographing may be accomplished with the use of a microscope or other magnifying lens.

By the term opacity as used herein with reference to a grain section is meant the appearance of the section when subjected'to examination in accordance with this invention and the opacity of sections will vary in accordance with the transmission, adsorption and/or reflection of light by the sections.

The term light" as used herein with reference to theexamination, appearance and/or opacity of grain sections is meant any form of radiant ugh, ordinary "white light isusually satory for examination of the sections, there the modifier used, in which the examination may be facilitated by employing monochromatic vie-- ible light, or light of selected wavelength in the invisible range, for instance in the ultra-violet or infra-red. When light outside of the visible range is employed for the examination, it is necessary to photograph the sections, or use some other suitable means, for instance a. fluorescent screen, for detecting the opacity of the sections.

It will be understood that while the treatment of gelatinous globular powder was described in the specific embodiment above, various other wwder and explosive bases may be employed'to secure the advantages of this invention. It will be further understood that various changes may be made in the specific details without departins-from the spirit and scope of this invention, and it is therefore to be understood that this invention is not to be limited by the detail described herein except as set forth-in the appended claims.

Having thus described the invention what is claimed is:

i. In the'manufacture of granular explosives, the process of controlling the treatment of explosive grains with a modifying agent which comprises preparing sections of representative grains, examining the sections to determine their opacity, and terminating said treatment when sections are obtained having an opacity indicating that the desired degree of modification has been accomplished. v

2. In the manufacture of granular explosives, the process of controlling the treatment of explosive grains with a coating agent which comprises grinding representative grains removed from the mass during said treatment to form thin sections thereof, examining said sections to determine their opacity, and terminating said treatment when sections are obtained having an opacity indicating that the desired coating has been accomplished.

3. In the manufacture of granular explosives, the process of controlling a treatment of powder grains which comprises preparing sections of said grains removed from the mass during said treatment, examining said sections, and terminating said treatment when sections are obtained having an opacity indicating that the desired modification ha been accomplished,

4. In the manufacture of granular explosives,

(I, the process of controlling a treatment for the removal of a solvent from powder grains in liquid suspension which comprises preparing thin sections of representative powder grains removed from the suspension during said treatment, examining the sections to determine their opacity, and terminating said treatment when sections are obtained having an opacity indicating that t e desired degree of solvent removal has been accomplished.

5. In the manufacture of granular explosives, the process of controlling a treatment of powder grains with a modifying agent which comprises grinding representative powder grains removed from the mass during said treatment to form uniformiy thin sections thereof, examining said sections to determine their opacity, and terminating said treatment when sections are obtained having an opacity indicating that the desired modification has been accomplished.

6. In the manufacture of granular explosives, the process which comprises treating powder grains in a liquid suspension with a modifying agent in the presenceof a solvent for said grains, treating said grains to remove said solvent therefrom, preparing uniformly thin sections of representative powder grains removed from the suspension during said solvent removal treatment,

examining said sections to determine the residual moval of solvent from powder grains in liquid suspension which comprises grinding representative powder grains removed from the suspension during said treatment to form uniformly thin sections thereof, examining said sections under the microscope to determine their opacity, and terminating said treatment when sections are obtained having an opacity indicating that the desired degree of solvent removal has been ac complished.

8. In the manufacture of granular explosives, the process which comprises treating powder grains in a liquid suspension with a modifying agent in the presence of a solvent for said grains, treating said grains to remove said solvent therefrom, gr nding representative powder grains removed ii i the suspension during said solvent iemo 'al treatment to form uniformly thin sections thereof, examining said sections to determine ti. eir opacity and terminating said solvent remove. treatment when sections are obtained having :El'l opacity indicating that the desired degree of solvent removal has been accomplished.

9. In the manufacture of granular explosives. the process of controlling a treatment for the coating of powder grains with a deterrent, which comprises preparing sections of representative grains, examining the sections to determine their opacity, and terminating said treatment when sections are obtained having an opacity indicating that the desired coating has been attained.

10. In the manufacture of granular explosives, the process which comprises heating powder grains containing volatile constituents in a liquid suspension, and controlling the removal of said volatile constituents from said powder grains by grinding representative powder grains removed from the suspension during said heating treatment, forming uniformly thin sections from said removed powder grains, examining said sections to determine their opacity, and terminating said heating treatment when sections are obtained having an opacity indicating that the desired removal of volatile constituents has seen accomplished.

ME'TON L. HERZOG.